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Code Manual for CONTAIN 2.0 - Federation of American Scientists

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Table 11-1<br />

Example Solution <strong>for</strong> Flow Path Initial Lengths in the Three-Node<br />

Representation <strong>of</strong> Suppression Pool Vents Shown in Figure 11-2<br />

Top Flow Path A = 17.8761<br />

L = 4.283<br />

Middle Flow Path A = 17.8761<br />

L = 6.490<br />

Bottom Flow Path A = 17.8761<br />

L = 8.362<br />

A = area (mz), L = inertial length (m), as represented in Equation (11-5), <strong>for</strong> L{z= 2.10, ~~ =<br />

~,= 1.27, ~, =~,=L~, = 1.52, and A1, =A,, =A,, =51.44 in Equation (11-1)<br />

11.1.2 Dedicated Suppression Pool Vent Flow Model<br />

The vent clearing and gas flow rate modeling <strong>for</strong> the dedicated model is discussed in this section.<br />

The architecture <strong>for</strong> this model is different from that <strong>of</strong> the multi-node model discussed above. First<br />

<strong>of</strong> all, only one suppression pool vent flow path maybe specified per problem. Secondly, in contrast<br />

to what one might expect, coolant is not actually exchanged between pools in different cells during<br />

the vent clearing process <strong>for</strong> this model. The reason is that the dedicated model uses only one pool,<br />

that in the wetwell cell, and assumes that this pool spans both the drywell and wetwell sides ~<br />

<strong>of</strong> the vent. Thus, the wetwell cell geometry and pool inventory should reflect the total pool volume<br />

and cross-section. Thirdly, the vent clearing calculation is carried out internally in the model to<br />

determine a vent clearing time, after which the vent is assumed to be accessible to gas flow. This<br />

vent clearing calculation keeps track <strong>of</strong> liquid levels that should be present on the @well and<br />

wetwell sides <strong>of</strong> the vent, on the basis <strong>of</strong> a quasi-steady liquid flow model. Note, however, that the<br />

wetwell pool level reported in the output is not just that <strong>of</strong> the wetwell side, but is an average value<br />

taking into account both sides <strong>of</strong> the vent. Other limitations <strong>of</strong> the single pool treatment are that gaspool<br />

equilibration in reverse flow is not modeled and flooding <strong>of</strong> the vent from the @well cell pool,<br />

if any, cannot be modeled properly.<br />

The dedicated suppression pool vent flow path is activated at the global level by the keyword<br />

SPVENT as described in Section 14.2.4.3 and can be used only in conjunction with the implicit flow<br />

solver option. (The implicit flow solver option is specified by the keyword IMPLICIT in the<br />

FLOWS input block, as described in Section 14.2.4.1.) With a vent flow path, two cells are required,<br />

one <strong>for</strong> the wetwell and one <strong>for</strong> the drywell. A pool must be specified as part <strong>of</strong> the lower cell input<br />

<strong>of</strong> the wetwell cell, and this pool should include both the drywell- and wetwell-side inventory. The<br />

area <strong>of</strong> the pool specified in the lower cell input <strong>for</strong> the wetwell cell should include all <strong>of</strong> the free<br />

surface associated with these inventones. Note that the inventory <strong>of</strong> aerosols, fission products, and<br />

dispersed core debris that have been scrubbed out <strong>of</strong> the gas passing through the pool is always<br />

associated with the wetwell pool or wetwell lower cell inventory.<br />

Rev O 11 8 6/30/97

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